Abstract

An equation for granulation kinetics has been derived on the basis of the mass balance of the material being granulated. The model presented takes into account mechanisms that cause a decrease in the mass of granule-size groups, i.e. crushing and abrasion, and mechanisms which lead to an increase in size group mass, i.e. coalescence and layering. Considering a given group of size distributions, a rate of mass fraction growth was presented taking into account the influence of granules of both larger and smaller size. As a result a dependence describing the increase in the mass fraction of a size group has been obtained. The dependence contains three characteristic functions: a decrement rate function for a given size group, an agglomeration rate function, and a function of the growth rate of a given size group resulting from destroying large-size granules (grinding rate function). An experimental granulation of wet fine material in a drum has been performed. The obtained granule-size distributions were approximated by a frequency function of gamma distribution. Theoretical size distributions were the basis for determining characteristic rate functions in a kinetic equation. As a result, all rate functions were described for each size group in the system during the whole granulation investigated. These functions completely described the kinetics of the granulation process. A comparison of real and theoretical distributions (determined on the basis of the model) obtained in subsequent periods of the process gives a good agreement of the model with the real run of the process.

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